US20020193640A1 - Polyethylene glycol and process for producing the same - Google Patents

Polyethylene glycol and process for producing the same Download PDF

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Publication number
US20020193640A1
US20020193640A1 US10/106,219 US10621902A US2002193640A1 US 20020193640 A1 US20020193640 A1 US 20020193640A1 US 10621902 A US10621902 A US 10621902A US 2002193640 A1 US2002193640 A1 US 2002193640A1
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Prior art keywords
glycol
polyethylene glycol
molecular weight
ethylene
diethylene glycol
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US10/106,219
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US6620976B2 (en
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Kenji Sakanoue
Kouzoh Sanchika
Tohru Yasukohchi
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NOF Corp
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NOF Corp
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    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G65/00Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule
    • C08G65/02Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule from cyclic ethers by opening of the heterocyclic ring
    • C08G65/26Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule from cyclic ethers by opening of the heterocyclic ring from cyclic ethers and other compounds
    • C08G65/2603Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule from cyclic ethers by opening of the heterocyclic ring from cyclic ethers and other compounds the other compounds containing oxygen
    • C08G65/2606Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule from cyclic ethers by opening of the heterocyclic ring from cyclic ethers and other compounds the other compounds containing oxygen containing hydroxyl groups
    • C08G65/2609Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule from cyclic ethers by opening of the heterocyclic ring from cyclic ethers and other compounds the other compounds containing oxygen containing hydroxyl groups containing aliphatic hydroxyl groups
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L2203/00Applications
    • C08L2203/02Applications for biomedical use

Definitions

  • This invention relates to a polyethylene glycol with low ethylene glycol and diethylene glycol contents which is to be used in fields with application to a living body such as the pharmaceutical field and the cosmetic industry, and a process for producing the same.
  • Polyethylene oxide which is a material generally obtained by polymerizing ethylene oxide, has inherent characteristics of being viscous, causing no irritation, being soluble in water and having lubricating properties. Owing to these characteristics, this compound has been widely used in water base paints, paper coatings, adhesives, printing inks, surfactants and the like.
  • polyethylene glycol serves as an important material in producing drugs and cosmetics in the fields with respect to a living body such as the pharmaceutical field and the cosmetic industry, since it has excellent solubility and compatibility.
  • polyethylene glycol compounds called “Macrogols” having different molecular weights are listed as official drugs in the Pharmacopoeia of Japan and employed as dissolution aids and fillers in various drugs and cosmetic materials.
  • Polyethylene glycol contains ethylene glycol and diethylene glycol the contents of which are specified to 0.25% (2,500 ppm) or less in the United States Pharmacopoeia etc., with respect to polyethylene glycols having a molecular weight of 1,000 or less for use in fields with application to a living body.
  • x represents the average molecular weight of the polyethylene glycol.
  • an object of the present invention is to provide a polyethylene glycol having an average molecular weight of from 190 to 1,050 for use in fields with application to a living body, wherein the sum of the contents of ethylene glycol and diethylene glycol is extremely low, and a process for producing the same.
  • x represents the average molecular weight of the polyethylene glycol and the polyethylene glycol has an average molecular weight ranging from 190 to 1,050;
  • polyethylene glycol having an average molecular weight of from 190 to 210 for use in fields with application to a living body, containing ethylene glycol and diethylene glycol in a total amount of 200 ppm or less.
  • the formula [I] above is a formula whereby the sum of the ethylene glycol and diethylene glycol contents in polyethylene glycol at each molecular weight is calculated.
  • the ethylene glycol and diethylene glycol contents at each molecular weight are appropriately selected depending on the requirements of an intended application. In case of use in fields with application to a living body, it is favorable from the viewpoint of toxicity that the sum of the ethylene glycol and diethylene glycol contents is 2,500 ppm or less at a molecular weight of 200. Since the sum of ethylene glycol and diethylene glycol contained in the material and the sum of ethylene glycol and diethylene glycol formed as by-products during the reaction decrease with an increase in the addition mole number of ethylene oxide, the sum of the ethylene glycol and diethylene glycol contents in the product amounts to a value calculated by multiplying by a definite decreasing ratio.
  • 150 represents the molecular weight of triethylene glycol and 2,900 represents a coefficient concerning the acceptable level of the ethylene glycol and diethylene glycol contents in the material.
  • (x-150)/44 means the addition mole number of ethylene oxide.
  • the decreasing ratio of the sum of the ethylene glycol and diethylene glycol contents per mole of ethylene oxide added is referred to as 0.85, the upper limit of the sum of ethylene glycol and diethylene glycol contained per mole (x g) of polyethylene glycol is thus indicated.
  • ethylene glycol and diethylene glycol levels are required.
  • polyethylene glycol having a low molecular weight of from 190 to 210 in particular, the sum of the ethylene glycol and diethylene glycol contents is desirably 200 ppm or less.
  • the present invention further provides a process for producing such a polyethylene glycol. More particularly, the present invention provides:
  • the polyethylene glycol provided by the present invention is a polyethylene glycol for use in fields with application to a living body which has an average molecular weight ranging from 190 to 1,050, and the sum of the contents of ethylene glycol and diethylene glycol is less or equal to that expressed by formula [I] below.
  • the polyethylene glycol provided by the present invention which is a polyethylene glycol having an average molecular weight ranging from 190 to 210 and the sum of the contents of ethylene glycol and diethylene glycol of less than or equal to that expressed by the following formula [I], still preferably 200 ppm or less, is highly useful. This is because there has been no polyethylene glycol meeting the standards as defined in the Pharmacopoeia of Japan and United States Pharmacopoeia and such a polyethylene glycol is in high demand in the market.
  • x represents the average molecular weight of the polyethylene glycol.
  • the upper limits at respective molecular weights calculated in accordance with the above formula [I] are as follows: 1,808 ppm in case of a polyethylene glycol having a molecular weight of 200, 833 ppm in case of a polyethylene glycol having a molecular weight of 300, 432 ppm in case of a polyethylene glycol having a molecular weight of 400, 138 ppm in case of a polyethylene glycol having a molecular weight of 600, and 19 ppm in case of a polyethylene glycol having a molecular weight of 1,000.
  • Preferred values at respective molecular weights are as follows: 200 ppm in case of a polyethylene glycol having a molecular weight of 200, 150 ppm in case of a polyethylene glycol having a molecular weight of 300, 100 ppm in case of a polyethylene glycol having a molecular weight of 400, 50 ppm in case of a polyethylene glycol having a molecular weight of 600, and 15 ppm in case of a polyethylene glycol having a molecular weight of 1,000.
  • a polyethylene glycol having the sum of ethylene glycol and diethylene glycol contents exceeding the level as defined by the above formula [I] is undesirable because of the excessively high content of impurities.
  • the lower limit of the sum of ethylene glycol and diethylene glycol contents may be 1 ppm or more in view of the detection limit of the measurement method.
  • the polyethylene glycol for use in fields with application to a living body is a physiologically useful polyethylene glycol. More particularly, it is a polyethylene glycol which is usable in products directly applied to the human body in fields with application to a living body such as drugs, cosmetics and toiletries. For example, it is useful as a medicinal base in dissolution aids, emulsifiers, dispersants, fillers, lubricating agents, etc., for injection preparations, external preparations, oral preparations and the like. Furthermore, it is useful as a cosmetic material for body cleansers such as toilet soaps, shampoos, rinses, facial cleansers and toothpastes and cosmetics such as cosmetic lotions, lotions, foundations, perfumes and lipsticks.
  • body cleansers such as toilet soaps, shampoos, rinses, facial cleansers and toothpastes
  • cosmetics such as cosmetic lotions, lotions, foundations, perfumes and lipsticks.
  • the polyethylene glycol provided by the present invention which has small ethylene glycol and diethylene glycol contents and an average molecular weight ranging from 190 to 1,050 can be produced by addition-polymerizing ethylene oxide to triethylene glycol in the presence of an alkali catalyst such as sodium hydroxide or potassium hydroxide.
  • an alkali catalyst such as sodium hydroxide or potassium hydroxide.
  • the triethylene glycol for use as a starting material is not restricted in purity, it is preferable to use triethylene glycol having a purity of 99.5% or more, still preferably 99.95% or more.
  • the triethylene glycol purity can be elevated by distilling, etc.
  • the alkali catalyst for use in the present invention is a strongly alkaline substance such as sodium hydroxide or potassium hydroxide. It is preferably added in an amount of from 0.005 to 1.0% by weight, still preferably from about 0.01 to 0.5% by weight, based on the triethylene glycol that is supplied.
  • the ethylene oxide addition-polymerization reaction is carried out preferably at a reaction temperature of from 80 to 230° C., still preferably from 120 to 180° C., and under a reaction pressure of from 0 to 1 MPa, still preferably from 0.2 to 0.6 NPa.
  • ethylene glycol and diethylene glycol as by-products can be suppressed, prior to the addition-polymerization of ethylene oxide to triethylene glycol, by heating triethylene glycol in a reactor to 70 to 150° C. and bubbling nitrogen gas under reduced pressure of 0 to 0.013 MPa for 0.5 to 3 hours to thereby eliminate water from the starting materials and the catalyst.
  • the ethylene glycol and diethylene glycol contents can be determined by the following method.
  • sample solutions 4 g portions of samples to be measured are each precisely weighed into a 10 ml container and 5 ml of the internal standard solution and 1 ml of distilled water are precisely added thereto. After capping, the mixture is well shaken.
  • WAX 52CB film thickness 1.0 ⁇ m
  • Carrier gas He (helium gas).
  • Injection temperature 250° C.
  • Injection volume 1 ⁇ l.
  • a response coefficient F N is calculated based on the peak areas obtained from the standard solution and each sample solution with the use of formula (1) below. Then, ethylene glycol and diethylene glycol are quantified using the formula (2).
  • C N concentration ( ⁇ g/ml) of ethylene glycol or diethylene glycol in the standard solution
  • r SI peak area of the internal standard obtained from the standard solution
  • C SI concentration ( ⁇ g/ml) of the internal standard in the standard solution.
  • r SN peak area of ethylene glycol or diethylene glycol obtained from the standard solution.
  • C I concentration ( ⁇ g/ml) of the internal standard in the internal standard solution
  • r N , r I peak areas of ethylene glycol or diethylene glycol and the internal standard obtained respectively from the sample solutions;
  • W weight (g) of each target substance in the sample solution.
  • the polyethylene glycol obtained by the present invention can be further processed by eliminating excessive ethylene oxide under reduced pressure and by eliminating the alkali catalyst by neutralizing the alkali catalyst with an acid such as phosphoric acid or hydrochloric acid or using an adsorbent.
  • antioxidants such as dibutylhydroxyltoluene and tocopherol may be added thereto depending on the intended purpose.
  • ethylene oxide was eliminated therefrom at 100C. under reduced pressure of 0.002 MPa for 1.5 hours. After cooling to 85° C., the mixture was neutralized by adding phosphoric acid and filtered to thereby give a target product (1) which was a polyethylene glycol having an average molecular weight of 202 (yield: 97%). When the obtained product was subjected to a smell test, no polyethylene glycol degradation smell was noticeable.
  • Example 2 After treating as in Example 1, a target product (2) which was a polyethylene glycol having an average molecular weight of 306 was obtained (yield: 95%). When the thus obtained product was subjected to a smell test, no polyethylene glycol degradation smell was noticeable.
  • Example 2 After treating as in Example 1, a target product (3) which was a polyethylene glycol having an average molecular weight of 406 was obtained (yield: 96%). When the thus obtained product was subjected to a smell test, no polyethylene glycol degradation smell was noticeable.
  • Example 2 After treating as in Example 1, a target product (5) which was a polyethylene glycol having an average molecular weight of 602 was obtained (yield: 95%). When the thus obtained product was subjected to a smell test, no polyethylene glycol degradation smell was noticeable.
  • the products of Examples 1, 2, 3 and 5 are polyethylene glycols respectively having molecular weights of from 190 to 210, from 285 to 315, from 380 to 420 and from 570 to 630 which were prepared using triethylene glycol as a starting material and dehydrating the triethylene glycol in a reactor before adding ethylene oxide.
  • the product of Example 4 is a polyethylene glycol having a molecular weight of from 190 to 210 which was prepared using triethylene glycol as a starting material and without dehydrating the triethylene glycol before the addition polymerization with ethylene oxide.
  • the ethylene glycol and diethylene glycol contents can be regulated to not more than the level defined by the above-described formula [I].
  • the sum of the ethylene glycol and diethylene glycol contents can be lessened to 200 ppm or less by dehydrating the starting material before the addition polymerization with ethylene oxide.
  • Comparative Examples 1 and 2 are polyethylene glycols each having a molecular weight of from 190 to 210 which were prepared using diethylene glycol as a starting material and dehydrating the diethylene glycol before the addition polymerization of ethylene oxide (Comparative Example 2) or without dehydrating (Comparative Example 1).
  • Comparative Examples 3 and 4 are polyethylene glycols each having a molecular weight of from 190 to 210 which were prepared using ethylene glycol as a starting material and dehydrating the ethylene glycol before the addition polymerization of ethylene oxide (Comparative Example 4) or without dehydrating (Comparative Example 3).
  • the product of Comparative Example 5 is a polyethylene glycol having a molecular weight of from 285 to 315 which was prepared using diethylene glycol as a starting material and without dehydrating the diethylene glycol before the addition polymerization of ethylene oxide.
  • Comparative Examples 6 and 7 are polyethylene glycols each having a molecular weight of from 380 to 420 which were prepared using diethylene glycol as a starting material and dehydrating the diethylene glycol before the addition polymerization of ethylene oxide (Comparative Example 7) or without dehydrating (Comparative Example 6).
  • the product of Comparative Example 8 is a polyethylene glycol having a molecular weight of from 570 to 630 which was prepared using diethylene glycol as a starting material and dehydrating the diethylene glycol before the addition polymerization of ethylene oxide.
  • the polyethylene glycol provided by the present invention can regulate the ethylene glycol and diethylene glycol contents to an extremely low level by using triethylene glycol as a starting material and addition polymerizing with ethylene oxide.
  • triethylene glycol as a starting material
  • addition polymerizing with ethylene oxide By dehydrating the triethylene glycol starting material in a reactor before the addition polymerization with ethylene oxide, the ethylene glycol and diethylene glycol contents can be regulated to a further lowered level.
  • the present invention provides a polyethlene glycol having the sum of the contents of ethylene glycol and diethylene glycol of less than or equal to that expressed by the following formula [I] and having an average molecular weight ranging from 190 to 1,050 adapted for use in fields with application to a living body such as medicinal preparations and cosmetics.
  • a polyethylene glycol having an average molecular weight of from 190 to 210 meets the standards for ethylene glycol and diethylene glycol contents as defined in the Pharmacopoeia of Japan or United States Pharmacopoeia.
  • x represents the average molecular weight of the polyethylene glycol.

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  • Chemical & Material Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Organic Chemistry (AREA)
  • Polyethers (AREA)
  • Medicinal Preparation (AREA)
US10/106,219 2001-03-27 2002-03-27 Polyethylene glycol and process for producing the same Expired - Lifetime US6620976B2 (en)

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JPP.2001-089455 2001-03-27
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JPP.2001-357035 2001-11-22
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Cited By (2)

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US20060069006A1 (en) * 2004-09-24 2006-03-30 Clariant Gmbh Polyethylene glycol and alcohol ethoxylates and their preparation
US20130280174A1 (en) * 2012-04-20 2013-10-24 The Gillette Company Personal care composition comprising metathesized unsaturated polyol esters

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ES2279374T3 (es) 2003-06-03 2007-08-16 Basf Aktiengesellschaft Procedimiento para la elaboracion de polialquilenglicoles de alta pureza.
DE10325264A1 (de) * 2003-06-03 2004-12-23 Basf Ag Hochreine Polyalkylenglykole und Verfahren zur Herstellung
DE10358213A1 (de) * 2003-12-12 2005-07-28 Clariant Gmbh Polyethylenglykol und dessen Herstellung
US7495063B2 (en) 2006-02-03 2009-02-24 Dow Global Technologies Inc. Reduced oligomer concentration in high purity polyalkylene glycols
CN102391493A (zh) * 2006-02-03 2012-03-28 陶氏环球技术有限责任公司 包含减少量的低聚物的聚烷撑二醇
EP1984422B1 (en) * 2006-02-03 2012-06-27 Dow Global Technologies LLC Polyalkylene glycols comprising a reduced amount of oligomers
CN101605751B (zh) 2007-01-23 2013-01-02 国际壳牌研究有限公司 制备烷二醇和二甲基碳酸酯的方法
WO2008090108A1 (en) 2007-01-23 2008-07-31 Shell Internationale Research Maatschappij B.V. Process for the preparation of an alkanediol and a dialkyl carbonate
CN101870728A (zh) 2009-04-23 2010-10-27 派格生物医药(苏州)有限公司 新型Exendin变体及其缀合物
WO2014089177A2 (en) 2012-12-04 2014-06-12 Massachusetts Institute Of Technology Compounds, conjugates and compositions of epipolythiodiketopiperazines and polythiodiketopiperazines
US10918627B2 (en) 2016-05-11 2021-02-16 Massachusetts Institute Of Technology Convergent and enantioselective total synthesis of Communesin analogs
US11932650B2 (en) 2017-05-11 2024-03-19 Massachusetts Institute Of Technology Potent agelastatin derivatives as modulators for cancer invasion and metastasis
US10640508B2 (en) 2017-10-13 2020-05-05 Massachusetts Institute Of Technology Diazene directed modular synthesis of compounds with quaternary carbon centers
CN110964116A (zh) 2018-09-26 2020-04-07 北京辅仁瑞辉生物医药研究院有限公司 GLP1-Fc融合蛋白及其缀合物
US11535634B2 (en) 2019-06-05 2022-12-27 Massachusetts Institute Of Technology Compounds, conjugates, and compositions of epipolythiodiketopiperazines and polythiodiketopiperazines and uses thereof
WO2022182415A1 (en) 2021-02-24 2022-09-01 Massachusetts Institute Of Technology Himastatin derivatives, and processes of preparation thereof, and uses thereof
WO2024086464A1 (en) * 2022-10-19 2024-04-25 Dow Global Technologies Llc Liquid polyethylene glycols

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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20060069006A1 (en) * 2004-09-24 2006-03-30 Clariant Gmbh Polyethylene glycol and alcohol ethoxylates and their preparation
US20130280174A1 (en) * 2012-04-20 2013-10-24 The Gillette Company Personal care composition comprising metathesized unsaturated polyol esters
CN104540493A (zh) * 2012-04-20 2015-04-22 吉列公司 包含复分解化的不饱和多元醇酯的个人护理组合物

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US6812367B2 (en) 2004-11-02
DE60200495T2 (de) 2005-05-19
EP1245608A1 (en) 2002-10-02
EP1245608B1 (en) 2004-05-19
US6620976B2 (en) 2003-09-16
US20030216602A1 (en) 2003-11-20
DE60200495D1 (de) 2004-06-24

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